Plug flow type bioleaching process and apparatus for sludge treatment

A bioleaching and plug-flow technology, applied in the field of environmental engineering, can solve problems such as poor sanitation, easy corruption, and small size, and achieve low investment and operating costs, improved flocculation and dehydration performance, and stable production processes.

Inactive Publication Date: 2009-08-12
NANJING AGRICULTURAL UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Their existence limits the rational utilization of sewage (silt) mud
[0008] 3. Due to the high content of organic matter, the sludge (silt) is easily corrupted, and there are many sulfur-containing substances (hydrogen sulfide, mercaptan, sulfide, etc.), ammonia or putrescine, low-molecular-weight volatile fatty acids, etc., and the stench is obvious; and usually contain a large number of pathogenic microorganisms, therefore, poor sanitation
However, reactors operated in batch mode (such as air lift type) are usually small in size, high in automation and technical requirements, and relatively large in investment and operating costs.

Method used

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  • Plug flow type bioleaching process and apparatus for sludge treatment
  • Plug flow type bioleaching process and apparatus for sludge treatment
  • Plug flow type bioleaching process and apparatus for sludge treatment

Examples

Experimental program
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Effect test

Embodiment 1

[0030] Example 1 Continuous push-flow bioleaching method for treating tannery sludge

[0031] According to the technique and equipment mentioned in the present invention, a set of continuous plug-flow bioleaching method is designed to process the technological process and equipment of sewage (silt) mud (see attached figure 1 ). In this project, the sewage (silt) sludge adjustment pond is 30m 3 , working volume of plug-flow bioleaching reactor is 100m 3 , advection concentration pool 10m 3 , recovery pool 20m 3 , activation pool 10m 3 , Roots blower power 5.5KW, wind pressure 39kpa, air volume 6m 3 / min; the dehydrator is a box-type filter press dehydrator (model XMG80 / 1000-U), with a filtration area of ​​80m 2 .

[0032] The organic waste for treatment is tannery sludge with a solid content of 2%-4% and a chromium content of 18000-31000mg / kg dry sludge. In the bioleach reactor, raw sludge is 3 / d amount into the reactor, press 5-10M at the same time 3 / d into the rec...

Embodiment 2

[0034] Example 2 Continuous push-flow bioleaching method for treating municipal sludge

[0035] Process flow and equipment facility are identical with embodiment 1. The organic waste for treatment is sludge from urban sewage treatment plants, the solid content is about 2-3%, and the heavy metal Cu content reaches 4500mg / kg dry mud, Zn2800mg / kg, Ni525mg / kg, Cd25mg / kg, Cr625mg / kg. In the bioleach reactor, raw sludge is 3 / d amount into the reactor, press 5-10M at the same time 3 / d into the reflux activated sludge after bioleaching, the sludge residence time in the reactor is 2-3 days, the pH of the bioleaching sludge at the sludge outlet drops below 2, and most of the heavy metals in the sludge are dissolved. After the sludge treated by bioleaching is further concentrated by gravity (with a water content of 93%), it is dehydrated with a chamber filter press (without adding any flocculant) to a water content of less than 65%. After this treatment, the removal rate of the abov...

Embodiment 3

[0036] Example 3 Treatment of livestock and poultry manure by continuous plug-flow bioleaching

[0037] Process flow and equipment facility are identical with embodiment 1. The organic waste for treatment is flushing livestock and poultry manure from large-scale pig farms, with a solid content of about 7-8%, heavy metal Cu content of 800mg / kg dry mud, Zn 544mg / kg, Cr 85mg / kg. For the convenience of treatment, before entering the bioleach reactor, the original flushing livestock and poultry manure is diluted in the adjustment tank to a solid content of less than 4%, and then press 10M 3 / d amount into the reactor, press 3-5M at the same time 3 / d into the reflux activated sludge after bioleaching treatment, the residence time of the livestock and poultry manure sludge in the reactor is 2 days, the pH of the bioleached manure at the sludge outlet drops below 3, and most of the heavy metals in the livestock and poultry manure Dissolution. After the manure treated by bioleachin...

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Abstract

The invention provides a plug-flow type bioleaching treatment process for sludge treatment and equipment thereof. The equipment comprises a sludge regulating reservoir, an activating tank, a plug-flow type bioleaching reactor, an advection type sludge concentrated tank, a heavy metal recovery pond and other facilities, an aeration device, a heating device, a dehydration device, a stirring device and other devices. The process comprises the following steps that: a sludge system is acidified by a composite bacterium consisting of a thiobacillus and an acid resistant heterotrophic bacterium under conditions of aerobism and existence of sulfur powder and other composite nutriments, heavy metal in the sludge is massively dissolved in liquid phase, the sludge is regulated at the same time so as to facilitate sedimentation and dehydration; the sludge stays in the reactor for 2 to 4 days; discharged treated sludge enters the concentrated tank to be subjected to gravity thickening; 20 to 50 percent of concentrated bioleaching sludge flows back to the reactor, and the rest sludge is subjected to chamber filtration and dehydration without adding any flocculating agent until the water ratio is below 60 percent; and the heavy metal in the water is recycled by an alkali precipitation method. The method can remove massive heavy metals of the sludge, has over 99 percent of sludge pathogen kill ratio, and ensures that the treated sludge does not have malodor and is in khaki color, thereby realizing the aims of innoxiousness and minimization of the sludge.

Description

1. Technical field: [0001] The invention relates to a method for removing heavy metals in organic waste such as municipal sewage (silt) sludge, industrial sewage (silt) sludge, river and lake sludge, livestock and poultry manure, improving dehydration performance, and realizing high dryness dehydration of sewage (silt) sludge. It belongs to the field of environmental engineering technology. 2. Technical background: [0002] According to statistics, by the end of March 2008, 1,320 urban sewage treatment plants had been put into operation across the country, with a treatment capacity of 97.25 million M 3 / day, there are 890 urban sewage treatment plants under construction, with a treatment capacity of 36.39 million tons / day, and the sewage (silt) sludge production rate is 1.5 dry tons of sewage (silt) sludge / 10,000 M 3 In terms of sewage, the current annual output of sewage (silt) mud in my country reaches 5.32 million tons of dry weight, which is equivalent to nearly 30 mill...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F11/02C02F11/12
CPCY02W10/20
Inventor 周立祥刘秀海廖岳华
Owner NANJING AGRICULTURAL UNIVERSITY
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